Submerged resistor type induction furnace



Augo 79 1945. M. TAMA ET AL SUBMERGED RESISTOR TYPE INDUCTION FURNACE 4 Sheets-Sheet 1 Original Filed Dec. 31, 1945 Aug. 7, 1945. M. TAMA ET AL 2,381,523

SUBMERGED RESISTOR TYPE INDUCTION FURNACE Original Filed Dec. 3l, 1943 4 Sheets-Sheet 2 IN VEN TOR. Md 02M Ange 7, 1945. M. TAMA ET AL 2,381,523

SUBMERGED RESISTOR TYPE INDUCTION FURNCE Original Filed Dec. 5l, 1945 4 Sheets-Sheet 3 p Xl Kmax

Aug. 7, 1945. M. TAMA ET AL 2,381,523

SUBMERGED RESISTOR TYPE INDUCTION FURNACE Originl Filed Dec. 51, 1945 4 Sheets-Sheet 4 I N VEN TOR.

Patented Aug. 7, 1945 SUBMEBGED RESISTOR FURNA Manuel Tama asslgnors to Trenton, N. J.

Original application Dec 516,518, now Patent No.

1945. Divided and this TYPE INDUCTION CE' and Marlo Tuna, Morrisville, Pa., Ajax Engineering Corporation,

einher 31,4943, Serial No.

2,375,049, dated May 1, application November 3, 1944, Serial No. 561,756 f 15 Claims.

The invention is a division of our copending patent application Ser. No. 516,518, filed, De-

cember 31, 1943, which has become Patent No. 2,375,049; it relates to an induction furnace of the submerged resistor type for melting metals.

A primary object, of the invention is to obtain superior metallic products which are free from slag inclusions.

Another object of the invention is to separate the slags particularly from molten metals 0f low specific gravity, such as aluminum, magnesium and alloys thereof.

Also an obiect of the invention is to obtain the separation of the slags from the molten metal in a quick and effective manner.

Another object of the invention is to effect the separation of the slags from the molten metals at places and zones of the melting channels which are easily accessible by cleaning tools from above, but to prevent the accumulation of the slags in parts o! the furnace which are only accessible with difllculty.

It is another important object of the invention to so force the slags in the easily accessible zones of the melting channels against the channel walls that they adhere to the same as a coherent paste.

It is animportant insure a continuous operation of submerged resistor type induction furnaces.

It is, therefore, also an object of the invention to avoid stoppages of the furnace operation and drainage of the furnace for the removal of the slags.

The physical principles upon which the invention is based, are the following:

When an electric current of a high density is forced to pass through a conductor-molten or solidit creates a magnetic field within the conductor and outside of it. Only the eld within the conductor produces forces beneficial for carrying out the invention.

The shape of this magnetic field is substantially the same when direct current or alternating current is used. By the combined effect of the current elements ilowing through the conductor and the magnetic ileld elements cutting through said current elements, internal forces are created within the conductor.

Ii the conductor is a molten metal, electromagnetic pressure gradients are established within the conductor with zones of high pressure at certain places and zones of low pressure at other places. The forces are directed towards the centers of the magnetic field and the object of the invention to direction of the forces can be determined by the well known three-finger rule. If alternating current is used, the direction of the forces is not changed when the current is reversed. Therefore, the pressure gradients created within the molten metal are always maintained in a deilnite direction during the entire process.

When non-conductiveA slag-particles are contained in the molten metal. the electromagnetic pressure gradients are only created in the molten metal surrounding the slag particles, while no forces are created inside the slag particles. The result is that the slag particles are pressed towards the zones of low hydrostatic pressure. in a direction opposite to the direction of the forces acting on the conducting liquid. The electromagnetic pressure gradients which can be created by the method here described may be about hundred times larger than those existing in a quiet mass oi' molten metal subjected only to gravity action.

The separation of slags from heavy metals, as for instance silicon steel, by the application of pressure gradients resulting from the combined action of a current passed through the molten silicon steel and the magnetic fields created thereby has already been suggested for openring induction furnaces where the primary coil is located above a ring of molten metal. The slag particles are expelled to the surface of the bath and removed therefrom. The instant invention-however, is not concerned with openring type induction furnaces.

Besides, the forced ilow oi the melt to the surface of the bath causes movements with incumbent inltration of air and oxidation, which is particularly harmful when easily oxidizable and light metals are molten.

It is also known to separate slags from molten metals by the combined forces created by the current passing through the molten mass and electro-magnetic fields produced by sources other than those normally produced by said current. The devices used in this known process for creating the external magnetic fields are either magnetic shields or solenoids, located outside of the lining holding the molten metal to be processed.

Furthermore, a separation of metal and slag and the expulsion of the same from the furnace has been attempted by the establishment oi two electromagnetic fields orientated to each other under cer-tain specific conditions. In this case currlnt is directly conducted into the molten met The invention relates to an induction furnace of thesubmerged resistor type. such as for instance described and claimed in U. B. Patent No. 2,339,964 ot Manuel Inma. U. B. Patent No. 2,342,617. of Manuel llama and Mario Tama. U. B. Patent No. 2,347,298. Re. 22.602 of Mario The furnaces described in these patents are provided with two types of melting channels so type channel into the second type channel and from the latter into the iirst type of melting channel is abruptly changed. The first type channels extend substantially vertical. and the second type channels extend substantially horizontal. The provision of these two types of channels is not novel as such. in induction furnaces. but they form. as afterwards explained, the basis for the instant invention which is not applicable to the customary one channel furnaces having a single curved continuous melting channel sometimes of equal, sometimes of gradually increasing and sometimes of gradually decreasing cross area extending from the one to the other hearth entering end.

In order to evaluate the forces and pressure Case l signmes a long conductor of circular cross-section carrying return conductor at a considerable distance away. in which case the center of the magnetic field coincides with the geometric center of the circle.

The magnetic lines of force are concentric circles around the geometric center M, Fig. 5. The field intensity at the center is nero and has a maximum value at the periphery. The highest electromagnetic pressure is created at the center and the lowest at the periphery. The forces are directed radially towards the center.

Case 2 signiiies an inlinitely long cylindrical coil creating a homogeneous magnetic neld in the cylindrical space it surrounds.

The magnetic lines of force are parallel to the axis of the coil. The heid intensity is zero at the outside layers o! the coil and has a maximum value at the inside layers. The highest electromagnetic pressure is created at the outside layers and the lowest at the inside layers. Non-conductive slag particles will, therefore, be deposited against the inside layers. The forces are directed radially towards the outside layers.

The conditions existing in the melting channels of the submerged resistor type of induction furnaces lie between the extreme cases Just discussed. as will be shown hereafter.

The internal forces produced by the mutual action oi electric current and magnetic fields in the manner described above, can be calculated from the equation K=0.1251.H (l) wherein K=force in dyn/cm.3

==current density in amp/cm.Il Hziield intensity in amp./cm.

a heavy current with the section the ileld intensity at the geometric ccnterisequaltoseroiseell'iguresand). The field intensity at the layer of a circle having the diameter s: will be Haw--z (2) Equationl in Equation l we iind unit of volume acting on all eleon a circle with the diameter :z

layers of the circular conductor By inserting the force per ments located In the outside the force is HIL-.XJ (5) By inserting Equation 5 into Equation l we find: Kx=0.125.z (6) At the inside laver we iind the maximum force per unit of volume:

Figure 'I shows a cross section of the conductor with the iieid lines m. and Figure 8 shows the distribution of the forces over the cross section.

In comparing Equation 4 with Equation 'l it will be seen that, under similar conditions. vis. equal current density and equal thickness of the conductor, the maximum force created at the inside layers is four'times larger in Case 2 than in Case i.

The conditions existing in the channels of submerged resistor type induction furnaces lie between the two extreme cases Just calculated. Figure 9 shows the primary coil A, the secondary conductor B of square cross section. the center line Y of primary and secondary and the stray iields m surrounding the secondary and cutting it. 'I'he zero point M oi' the neld is located inside of the secondary but not in its center, as in Case l. It is also more inside of the conductor B than in Case 2. The values of maximum forces will. therefore, lie between those given by Equations 4 and 7. 'I'he forces created in an assembly according to Figure 9 cannot be determined by analytic means; but they may be calculated by graphical Integrations, after measuring and plotting the intensity of the stray tield.

However, it is not necessary to enter deeper into this complicated procedure, because the current density and the thickness or cross area of the conductor are the determining factors. and it is possible to formulate a simple rule in order to obtain the beneiits of the method steps called for by the present invention, as will be shown shortly hereafter.

Based on the above described principles the invention mainly resides in the provision of two type melting channels which act diiferently to wards the slag particles suspended in the molten conductor and transported by its now force through these channels.

The first channel type which preferably extends in a substantially vertical direction has a strongly reduced cross area in comparison with the second type channel which preferably extends in a substantially horizontal direction. The reduced cross area is provided in a part or zone of the first type melting channels which is easily accessible by cleaning tools from above and is preferably located in the upper end section of the channels. Due to the difference of the cross area in those two types of melting channels electromagnetic pressure gradients are created in the first named channel type of such magnitude that the slags suspended in the molten conductors are forced out of the same and pressed against the channel walls to which they strongly adhere; here they form a coherent paste and can be easily removed by the insertion of cleaning tools from above; the furnace remains filled with the molten charge and no interruption occurs of its operation.

In the second type channel the cross area is so enlarged in comparison to the first type channels and the electromagnetic pressure gradients therefore are so small that they are overcome by the flow force of the molten conductor, therefore slags do not adhere to the channel walls, but are conducted into the first type channels where they are trapped and pressed against the walls, as described in the foregoing.

From the above given explanation it is obvious that submerged resistor type induction furnaces provided with one continuous melting channel even having gradually decreasing or gradually increasing cross areas cannot be used for the perfomance of the invention as the provision of two types of melting channels having an abruptly changed flow direction and a different cross area is a prerequisite oi the invention.

The sizes of the cross areas of the two types of melting channels are apparent from the previously given theoretical deductions and can be easily determined if the following rules are applied.

Referring now again toV Equations 4 and 7 which show that the pressure gradients are pro-y portional to the product :P D of current density and thickness of the conductor, it was found that a particularly satisfactory concentration of the slag particles may be obtained in the melting channels of the furnace, if this product is essentially equal to or larger than 3x106 and that the slag deposits do not occur if the said product is equal to or less than 037x106.

If the cross area of the conductor is circular, D

represents its diameter; if the cross-section is not circular, D represents the diameter of a circle having the same area as the non-circular conductor, or in other words, the cross area of the circle lto which the non-circular cross area is reduceable; for the sake of .simplicity D will henceforth be called reduced diameter.

The following examples will serve to further illustrate the use of this simplified rule:

Example 1 In a furnace similar to the one shown in Figure 2, the two lateral vertical channels of circular cross-section have a diameter of 5 cm. and carry a current of 17,500 amps. each; the product j2.D is 4X 106; the slag particles are pressed to the walls on this tubular channel and can be easily removed therefrom.

The central vertical channel of the same furnace has al rectangular cross section of 5cm. l0 cm. and carries a current of 35,000 amps.; the product 9'2.D is 31x10, The intensity of the slag deposition is slightly reduced in comparison to the two lateral channels.

The bottom channel of the same furnace has a rectangular cross section of 71/2 cm. 10 cm. and carries a current of 17,500 amps.; the product 7'2.D is equal to 053x106. No slag deposition mok place in this bottom channel after a continuous operation of the furnace of more than 6 months.

Example 2 In a furnace similar to the one shown in Fig. l, the vertical channels have a cross-section of 6.7 cm. 6.7 cm.` and carry a current of 31,000 amps. The product :f2.D is equal to 3.6)(106. A satisfactory deposition and adherence of the slag particles results on the walls of the vertical channels.

The bottom channel of the same furnace consists of two superposed parts; the upper one having a. rectangular cross-section of 6.4 cm. 7.5 cm. above, and the lower one having a rectangular cross section of 7.5 cm. l2.5 cm. The current carried by the conductor in this channel is 31,000 amps.; the product i2.D is equal to 0154x106, No slag deposits occurred in this channel.

In computing these figures the current density should be expressed in amp./cm.2 and the reduced diameter in centimeters. The current should correspond to the maximum power of the furnace. Inasmuch as the product 7'2.D does not give the exact amount of pressure gradient but is intended to be used only as a guide for the disposition of the melting channels, it is not necessary to attach any dimension to it. However, the following figures will demonstrate that very high pressures are necessary to obtain the effects described in the present invention.

In the vertical channels of the furnacereferred to in Example l, the maximum 4pressure gradients are 125,000 dyn/cm.3 (or 127.5 gr./cm.3), according to Equation 4, and 500,000 dyn/cm.3 (or 510 gr./cm.3) according to Equation 7. Inasmuch as the specific gravity of aluminum is 2.7 gr./cm.3,the forgoing pressure gradients are from 47 to 188 times larger than those created by gravity action alone. The actual pressures existing in the melting channels of submerged resistor induction furnaces lie between these two magnitudes, as explained above.

Best results are obtained when the ratio of the cross-sectional area ofthe bottom channels to that of the vertical channels is approximately 3:1. If this rule is followed, the ratio of the electromagnetic pressures in the bottom channels to that of the vertical channels is approximately 1:5,

The progress due to this invention is particularly apparent in the melting of light metals in submerged resistor type induction furnaces.` Up to the present time no induction furnaces of this type have been operated for the melting of these metals in a continuous manner.

Experiments carried out twenty years ago by one of the applicants in melting aluminum alloys in a standard induction furnace for brass revealed that the furnace could be kept in operation only from 3 to 4 hours. After breaking the furnace lining and inspecting the melting channels, it was discovered that the bottom parts of the channels had been completely contaminated with non-conductive oxides, which increased their resistance to such a degree that no power could be absorbed by the furnace; these trials were repeated several times and finally given up, because a continuous operation could not be obtained.

At a later date submerged resistor type induction furnaces for melting light metals were made with arcuated melting channels of very large cross-section. In order to keep these furnaces in operating condition it was necessary to discharge the molten metal from the furnace into the ladle, to remove the slags from the channels with flexible chains while the lining was hot and to charge the furnace again with the molten metal contained in the ladle. This, of course, was a serious disturbance of the melting operation, which required 20 to 30 minutes interruption of the melting process and had to be repeated at intervals ranging from 8 to 24 hours.

Further -progress was made at a later date when the furnaces were provided with one or more removable plugs at the bottom for the purpose of cleaning the lower parts of the melting channels ai'ter the furnace was drained` But again a continuous operation was not obtained, because the charge had to be removed in order to proceed with the reconditioning of the furnace.

Following the teachings of the present invention it is possible to obtain the concentration and deposition of the slag particles at desired places within the molten bath which are easily accessible and to prevent this phenomenon at places where they are harmful for the operation and could only be removed with dimculty and after emptying the furnace.

'Ihe present furnace may be operated in a substantially continuous manner, using at all times the full power and interrupting the operation only for the purpose to charge and to discharge the metal.

Furnaces of the type described in the present application have been used for melting aluminum alloys in a continuous manner at different foundries in the United States for a period of from three to iive months without the necessity of interruption for cleaning the bottom channels, whereas under the hitherto customary conditions the same furnace would have to be stopped after several hours of work.

'I'he invention which renders it possible to continuously melt slag containing metals and particularly light metals and alloys in a submerged resistor type induction furnace, therefore. signifles an outstanding progress in the art.

Zones which answer the requirement of an efflcient slag concentration and easy accessibility without drainage of the furnace are vertical or substantially vertical melting channels where pressure gradients of the here desired magnitude are created.

Under the action of these electromagnetic pressure gradients the non-conductive slag particles are pressed and pasted against the walls of these easily accessible sections of the melting channels where the greatest force Km is created. 'I'hese zones ot a maximum force correspond with those of maximum pressure gradients because the pressures are the integral of the forces and vice versa, the forces are the differentials of the pressures. It will be noted that the forces were expressed (Equation 1) in dyn/cm.s and that the pressures which are expressed in terms of dyn/cm.2 must be divided by the unit oi' length in order to obtain the force.

assunse 'Ihe force K, according to Equation 1, therefore determines the pressure gradient at a certain point.

Submerged resistor induction furnaces for the successful operation of the invention are illustrated by way of example in the attached drawings.

Fig. 1 to Fig. 4 show vertical sectional elevations of several forms of furnaces constructed in conformity with this invention.

Figures 5 to 9 are schematical views to support the matematical explanation upon which the invention is based.

The furnace shown in Fig. l comprises a hearth 2 and a secondary loop composed of bottom channel I and vertical melting channels 6; the furnace is surrounded by a casing i which is provided with a refractory lining 3. The secondary loop is threaded by a primary composed of iron core 4 and coil l which is insulated by an asbestos sleeve l.

The cross area of the vertical melting channels I is slightly tapered in an upward direction; maximum forces and correspondingly maximum pressure gradients are created in the upper end sections l where the slag particles are concentrated and where they are caused to strongly adhere to the inside walls of the melting channels; the upper end sections l may be made cylindrical to facilitate the cleaning thereof.

'I'hese zones of maximum force are easily accessible from above. The slags may be removed from the same continuously or intermittently by the introduction of tubular cleaning tools of gradually increasing diameter, which cut out accordingly shaped slag rings. The melting channels are thereby kept free for the full passage of the current. If reconditioning of the melting channels is needed, it can be easily carried out.

In the horizontal channel 5 which has a large cross-section compared with the vertical channels and correspondingly lower pressure gradients no accumulation, concentration or deposition of slags occurs in spite of greatly extended periods of furnace operation, because these slags, which due to the insuilicient magnitude of the electromagnetic pressure gradients produced in this channel do not adhere to the walls thereof, are carried therefrom by the flow velocity of the conductor and concentrated in the vertical channels 8 where high magnitude pressure gradients prevail.

'I'his phenomenon is astounding in submerged resistor type induction furnaces provided with vertical and horizontal melting channels as hitherto experience has proven that the slags tend to deposit and to accumulate in furnaces of this type in the horizontal melting channel only; this channel therefore had to be cleaned which necessitates the previously mentioned tiresome and expensive stoppages of the furnace opera- It is obvious from the explanation given above that the full advantage of the invention can best be materialized in a submerged resistor type induction furnace where the secondary loop is composed of a substantially horizontal bottom channel and a plurality of substantially straight vertical melting channels connecting the hearth with the bottom channel. The ratio of the cross area of the bottom channel 3 to the next adiacent cross area. i0 of the vertical channels 6 may be preferably maintained at about 3:1.

The furnace embodied in Fig. 2 oi' the drawings is different from the one shown in Fl'g. 1 of the drawings insofar as three vertical melting channels of preferably circular shape, viz. a central channel Il and two lateral channels 6 are used; corresponding elements of the furnace are designated with same numerals as in Fla. l.

In the modification of the invention shown in Fig. 3 baille plates Il of a refractory material are located on top of `the vertical melting channels 6. The zones of maximum hydrostatic pressure gradients are chiefly located in the passages I3 between the baille plates I4 and the bottom of the hearth. In order to clean the furnace the plates may be lifted whereby the passages I3 are made easily accessible.

In the furnace shown in Fig. 4 inserts I5 are located in upper end sections of the vertical melting channels 6. The central passages IB provided in these inserts signify the slag concentrating zones of maximum electromagnetic pressure gradients.

In carrying out this invention the vertical channels may be cleaned from adhering slags or I dross by using tubular straight tools of steel;

preferably heat resisting steel having the same shape as the melting channels. It is advisable to use several sets of tools, one fitting exactly to the full cross section of the channels and the others having slightly smaller cross sections, andto use the smallest tool first and the larger ones subsequently. `The slags are caught at the inside of these tubular tools. This cleaning operation may be performed while the furnace is fully charged.

The invention has been described with particular reference to the melting of light metals and light metal containing alloys.

Alloys, such as for instance aluminum bronzes and copper-aluminum silicon alloys may also be successfully molten according to this invention.

Due to the complete separation of the suspended slag particles from the melt superior castings are obtained by the use of the present furnace.

The invention is in no way restricted to the furnace and melting channel structures shown to illustrate the principles upon which the same is based and many modifications may become evident to those skilled in the art to obtain part or all of the benefits of the invention; therefore. we claim all such furnace structures insofar as they fall within the reasonable spirit and scope of the invention.

Having thus described the same what we claim as new is:

1. A submerged resistor type induction furnace for melting metals comprising in a casing an upper melting hearth, a secondary loop underneath the said melting hearth, a transformer assembly threading the secondary loop, the said loop including a plurality of melting channels so arranged that the flow direction of the molten conductor during the transition from one channel into a second `melting channel is abruptly changed, zones in a part of the melting channels easily amenable by cleaning tools from above, said zones having a reduced cross area to crea-te therein by the combined action of a high current density and the resulting electromagnetic fields electromagnetic pressure gradients of a magnitude to cause slag particles suspended in the melt to be pasted to the zone walls whereby the slags may be easily removed from the' said walls while maintainingthe furnace in operation.

2. A submerged resistor type induction furnace for melting metals comprising in a casing an upper melting hearth, a secondary loop -underneath the said melting hearth, a transformer assembly threading the secondary loop, the said loop including a plurality of substantially vertical and a substantially horizontal melting channel, zones in the said vertical melting channels easily amenable by cleaning tools from above, said zones having a reduced cross area to create therein by the combined action of a high current density and the resulting electromagnetic fields electromagnetic pressure gradients of a magnitude to cause slag particles suspended ln the melt to be pasted to the zone Walls whereby the slags may be easily removed `from the said Walls while maintaining the furnace in operation.

3. A submerged resistor type induction furnace for melting metals comprising in a casing an upper melting hearth, a secondary loop underneath the said melting hearth, the said loop including two types of melting channels, the first type being easily amenable -to cleaning tools from above and having a reduced cross area to create by the combined action of high current density and the resulting electromagnetic fields electromagnetic pressure gradients of a magnitude to cause the slag particles suspended in the melt to adhere to the channel walls, the second type melting channel diilicuitly amenable to cleaning tools from above having an enlarged cross area to exclude due to the insufficient magnitude of the therein created electromagnetic pressure gradients and due to the flow force of the molten conductor a deposition of the slag particles at its walls.

4. A submerged resistor type induction furnace for melting metals comprising in a casing an upper melting hearth, a secondary loop underneath the said melting hearth, the said loop including tw`o types of melting channels so arranged that the flow direction of the molten conductor from the one type melting channels into the second type melting channel and from the latter into the rst type of melting channels is abruptly changed, the first type being easily amenable to cleaning tools from above and having a reduced cross area to create by the combined action of high current density and the resulting electromagnetic elds electromagnetic pressure gradients of a magnitude to cause the slag particles suspended in the melt to adhere to the channel walls, the second type melting channel diicultly amenable to cleaning tools from above having an enlarged cross area to exclude due to the insufficient magnitude of the therein created electromagnetic pressure gradients and due to the flow force of the molten conductor a deposition of the slag particles at its walls.

5. A submerged resistor type induction furnace for melting metals comprising in a casing an upper melting hearth, a secondary loop underneath the said melting hearth, a transformer assembly threading the secondary loop, the said loop including a plurality of substantially vertical and a substantially horizontal melting channel so arranged lthat the flow direction of the molten conductor during the transition from one channel into a second melting channel is abruptly changed, zones in the said vertical melting channels easily amenable to cleaning tools from above, said zones having a reduced cross area to create of a paste, the substantially horizontal melting channel being dimcultly amenable to cleaning tools from above having an enlarged cross area to exclude due to the insufiicient magnitude of the therein created electromagnetic pressure gradients and due to the flow force of the molten conductor a deposition of the slag particles at its walls. V

6. A submerged resistor type induction furnace for melting metals comprising in a casing an upper melting hearth, a secondary loop underneath the said melting hearth, the said loop including two types of melting channels, the ilrst type being easily amenable to cleaning tools from above and having a reduced cross area to create by the combined action of a high current density and the resulting electromagnetic ilelds in the melt to adhere to the channel walls, the second type melting channel being dimcultly amenable to cleaning tools from above having an enlarged cross area to exclude due to the insumcient magnitude of the therein created electromagnetic pressure gradients and due to the flow force of the moltenconductor a deposition of the slag particles at its walls.

7. A submerged resistor type induction furnace for melting metals comprising in a transformer assembly threading the secondary loop, the said loop including a plurality of substantially vertical and a substantially horizontal melting channel so arranged that the flow direction of the molten conductor during the transition from one channel into a second melting channel is abruptly changed, zones in the said vertical melting channels easily amenable to cleaning tools from above, said zones having a reduced cross area to create therein by the combined action oi a high cui-- rent density and the resulting electromagnetic ilelds electromagnetic pressure gradients` of at least a magnitude of j :3.104i to cause the slag particles suspended in the melt to adhere as a paste to the channel walls, the substantially horiable to cleaning tools from above having an enlax-ged cross area to exclude due to a maximum magnitude of 12D=0.6x 10 of the therein created electromagnetic pressure gradients and due to the now force of the molten conductor a deposition of the slag particles at its walls.

8. In an induction furnace according to claim 3 the first type melting channels extending in a substantially vertical direction and having an upwardly tapered cross area.

9. In an induction furnace according to claim 3 the first type melting channels consisting of three channels extending in a substantially vertical direction, the center channel having a substantially equal cross area and the two side channels having an upwardly tapered cross area, the second type channel extending in a substantially horizontal direction and being connected with all three first type melting channels.

l0. In a furnace according to claim 3 the ratio of the cross areas of the second type substantially horizontal melting channel to the next adjacent cross area o: the first type substantially vertical melting channels being about 3:1.

l1. In a furnace 12. Inafurnaceaccordingtoclaimstbeslag collecting sones being formed of substantially refractory bodies removably inserted into the upper ends of the substantially vertical melting channels. said bodies having inner cylindrical center passages.

13. In a furnace according to claim l the amenable parts of the melting channels having a circular cross section.

14. A submerged resistor type induction furnace for melting metals comprising in a casing an upper melting hearth, a secondary loop underneath the said melting hearth, the said loop including two types of melting channels. the first type being easily amenable to cleaning tools from above and having a circular reduced cross area to create by the combined action of high current density and the resultingelectromagnetic fields electromagnetic pressure gradients of a magnitude to cause the slag particles suspended in the melt to adhere to the channel walls, the second type melting channel diillcultly amenable to cleaning tools from above having an enlarged cross area to exclude due to the insuillcient magnitude of the therein pressure gradients and created electromagnetic due to the flow force of the molten conductor a deposition of the slag particles at its walls.

l5. In a submerged resistor type induction furnace a secondary having a bottom portion and area to prevent at a given current density the deposition ot non metallic components and to thereby maintain their suspension in the ilow of the melt.

MANUEL TAMA. MARIO TAMA. 

